Fed-Batch - Polyhydroxyalkanoates Production in KT2440 and Δ Mutant on Biodiesel-Derived Crude Glycerol.

Crude glycerol has emerged as a suitable feedstock for the biotechnological production of various industrial chemicals given its high surplus catalyzed by the biodiesel industry. bacteria metabolize the polyol into several biopolymers, including alginate and medium-chain-length poly(3-hydroxyalkanoates) (PHAs). Although is a suited platform to derive these polyoxoesters from crude glycerol, the attained concentrations in batch and fed-batch cultures are still low. In this study, we employed KT2440 and the hyper-PHA producer Δ mutant in two different fed-batch modes to synthesize -PHAs from raw glycerol. Initially, the cells grew in a batch phase (μ 0.21 h) for 22 h followed by a carbon-limiting exponential feeding, where the specific growth rate was set at 0.1 (h), resulting in a cell dry weight (CDW) of nearly 50 (g L) at 40 h cultivation. During the PHA production stage, we supplied the substrate at a constant rate of 50 (g h), where the KT2440 and the Δ produced 9.7 and 12.7 gPHA L, respectively, after 60 h cultivation. We next evaluated the PHA production ability of the strains using a DO-stat approach under nitrogen depletion. Citric acid was the main by-product secreted by the cells, accumulating in the culture broth up to 48 (g L) under nitrogen limitation. The mutant Δ amassed 38.9% of the CDW as -PHA and exhibited a specific PHA volumetric productivity of 0.34 (g L h), 48% higher than the parental KT2440 under the same growth conditions. The biosynthesized PHAs had average molecular weights ranging from 460 to 505 KDa and a polydispersity index (PDI) of 2.4-2.6. Here, we demonstrated that the DO-stat feeding approach in high cell density cultures enables the high yield production of -PHA in strains using the industrial crude glycerol, where the fed-batch process selection is essential to exploit the superior biopolymer production hallmarks of engineered bacterial strains.